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Process Equipment and Plant Design

Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

0.01 to 1
1.5 to 2.5
5 to 10
10 to 20

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Process Equipment and Plant Design
A high vapour velocity is required for high plate efficiency in a seive plate coloumn. The satisfactory value of operating vapor velocity for design purpose in seive plate column is about __________ percent of the flooding velocity.

95
80
60
45

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Process Equipment and Plant Design
The wall thickness of thin cylindrical shell with hemispherical ends is __________ that of the spherical ends.

Either B or C; depends on maximum permissible internal pressure
Less than
Equal to
More than

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Process Equipment and Plant Design
Slope of countercurrent flow rotary drier is in the range of __________ meter/metre.

0 to 1.5
0 to 2.2
0 to 0.08
0 to 0.8

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Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Remains same
Increases
Remains same, only if the number of tube passes does not change
Decreases

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Process Equipment and Plant Design
In a multipass shell and tube heat exchanger, the baffles on shell side is primarily provided for

Reducing scale deposition
Increasing pressure drop
Fixing the tubes
Creating turbulence

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